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Method for preparing fluorinated polyimide film for separating arene/alkane through permeating and steaming

A polyimide membrane, polyimide technology, applied in separation methods, semi-permeable membrane separation, chemical instruments and methods, etc., can solve problems such as complex processing processes and achieve good separation effects.

Inactive Publication Date: 2009-07-01
山东蓝景膜技术工程有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the prior art, most of the diamine monomers used are 2,4,6-trimethyl-1,3-phenylenediamine or 3,5-diaminobenzoic acid (such as Xu WY, et al. , J Membr Sci, 2003, 219, 89-102), such a membrane has a relatively large volume and polarity of the side groups, resulting in a tight arrangement of molecules, and only when the content of aromatic hydrocarbons is relatively high can it show a large permeability. amount, and it must be cross-linked to inhibit swelling, and the processing process is complicated

Method used

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  • Method for preparing fluorinated polyimide film for separating arene/alkane through permeating and steaming
  • Method for preparing fluorinated polyimide film for separating arene/alkane through permeating and steaming

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] Add 110ml of DMAc (N,N-dimethylacetamide, processed by vacuum distillation before use) and 10g of diamine monomer BDAF (2,2-bis[4 -(4-aminophenoxy)phenyl]hexafluoropropane) (vacuum high-temperature dehydration before use), after the diamine monomer is completely dissolved to form a transparent solution, add 8.57g of dianhydride monomer 6FDA (4,4' -hexafluoroisopropylidene-phthalic anhydride) (purify by sublimation before use). After the reactant was completely dissolved at room temperature to form a homogeneous solution, it was moved to react in an ice-water bath for 12 hours, and then 8 g of acetic anhydride and 1.2 g of triethylamine were added with a pipette for imidization reaction for 18 hours, and the final The obtained viscous polyimide solution was poured into deionized water to precipitate out, and then taken out after repeated washing, and dried at 150° C. for 10 hours to remove the solvent to obtain the product fluorine-containing polyimide 6FDA-BDAF.

[003...

Embodiment 2

[0045] Obtain 6FDA-BDAF material according to the operation of Example 1.

[0046] 9g of 6FDA-BDAF was dissolved in 95g of NMP, and dissolved under magnetic stirring for 24 hours to obtain a uniform and transparent polyimide solution. After the casting solution was filtered to remove impurities, vacuum defoaming was performed for 1 hour.

[0047] Cast the membrane solution on clean glass, place it under an infrared lamp to evaporate the solvent for 3 hours, take it out, and soak it in water at room temperature for 2 hours. Finally the membrane was taken out of the water and the polyimide membrane was peeled off the glass plate. The polyimide film 6FDA-BDAF thus obtained had a thickness of 17 μm.

[0048] This membrane was used to test the pervaporation separation performance of aromatics / alkanes. The feed was a toluene / n-heptane mixture with a toluene mass content of 20%. At 85°C, the permeation flux was 1.27kg·μm·m -2 h -1 , the separation factor is 4.36.

Embodiment 3

[0050] Obtain 6FDA-BDAF material according to the operation of Example 1.

[0051] 9g of 6FDA-BDAF was dissolved in 95g of DMF, and dissolved under magnetic stirring for 24 hours to finally obtain a uniform and transparent polyimide solution. After the casting solution was filtered to remove impurities, vacuum defoaming was performed for 1 hour.

[0052] Cast the membrane solution on clean glass, place it under an infrared lamp to evaporate the solvent for 2.5 hours, take it out, and soak it in water at room temperature for 2 hours. Finally the membrane was taken out of the water and the polyimide membrane was peeled off the glass plate. The polyimide film 6FDA-BDAF thus obtained had a thickness of 17 μm.

[0053] This membrane was used to test the pervaporation separation performance of aromatics / alkanes. The feed was a toluene / n-heptane mixture with a toluene mass content of 20%. At 85°C, the permeation flux was 0.64kg·μm·m -2 h -1 , the separation factor is 3.52.

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Abstract

A fluorine-containing polyimide membrane preparation method for separation of infiltration vaporization aromatic hydrocarbon / alkane belongs to the infiltration vaporization aromatic membrane separation technical field. The prior polyimide membrane must carry out the crosslinking to restrict the swelling, with complex disposal process. The invention includes 1) synthesis of the fluorine-containing polyimide: the diamine monomer is added to the solvent on the condition of nitrogen and mixing and is then fully dissolved; after that, the dianhydride monomer 6FDA is added to carry out the polycondensation for 12 through 18 hours; after that, the acetic anhydrite and the triethylamine are added for the imidization reaction, and the final outcome is deposited in the water, which is dried for reserve; 2) preparation of the casting solution is as following: the uniform casting solution is dissolved in the solvent, filtrated and defoamed; 3) membrane scraping: the membrane is formed by flow casting on the glass plate. The fluorine-containing polyimide uniform membrane can be obtained after the solvent is volatile after 2 through 3 hours and dipped in the water for 1 through 2 hours. The invention has the advantages of simple process, good heat and chemical stability, mechanical performance of the selected material, and good separation effect.

Description

Technical field: [0001] The invention relates to a preparation method of a fluorine-containing polyimide membrane that can be used for the separation of pervaporation aromatic hydrocarbons / alkanes, and belongs to the technical field of pervaporation membrane separation. Background technique: [0002] Pervaporation, or pervaporation (PV for short), is a new membrane technology for the separation of liquid (gas) and gas mixtures. It is driven by the partial vapor pressure of the components in the liquid mixture, and uses the different dissolution and diffusion speeds of the components through the dense film to achieve separation. Its outstanding advantage is that it can achieve distillation, extraction and absorption with low energy consumption. Separation tasks that are difficult to achieve with traditional methods. In the application of pervaporation technology, the separation of aromatics / alkane system is one of the most challenging issues, which is of great significance i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D71/46B01D53/22
Inventor 李继定叶宏陈剑林阳政
Owner 山东蓝景膜技术工程有限公司